EP1196346B1 - Method for filling a container - Google Patents

Method for filling a container Download PDF

Info

Publication number
EP1196346B1
EP1196346B1 EP00949609A EP00949609A EP1196346B1 EP 1196346 B1 EP1196346 B1 EP 1196346B1 EP 00949609 A EP00949609 A EP 00949609A EP 00949609 A EP00949609 A EP 00949609A EP 1196346 B1 EP1196346 B1 EP 1196346B1
Authority
EP
European Patent Office
Prior art keywords
weight
substance
time
filling
receptacle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP00949609A
Other languages
German (de)
French (fr)
Other versions
EP1196346A1 (en
Inventor
André Graffin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Serac Group SAS
Original Assignee
Serac Group SAS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Serac Group SAS filed Critical Serac Group SAS
Priority to DK00949609T priority Critical patent/DK1196346T3/en
Publication of EP1196346A1 publication Critical patent/EP1196346A1/en
Application granted granted Critical
Publication of EP1196346B1 publication Critical patent/EP1196346B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01GWEIGHING
    • G01G13/00Weighing apparatus with automatic feed or discharge for weighing-out batches of material
    • G01G13/24Weighing mechanism control arrangements for automatic feed or discharge
    • G01G13/28Weighing mechanism control arrangements for automatic feed or discharge involving variation of an electrical variable which is used to control loading or discharge of the receptacle
    • G01G13/285Weighing mechanism control arrangements for automatic feed or discharge involving variation of an electrical variable which is used to control loading or discharge of the receptacle involving comparison with a reference value
    • G01G13/2851Weighing mechanism control arrangements for automatic feed or discharge involving variation of an electrical variable which is used to control loading or discharge of the receptacle involving comparison with a reference value for controlling automatic loading of weigh pans or other receptacles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67CCLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/20Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus with provision for metering the liquids to be introduced, e.g. when adding syrups
    • B67C3/202Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus with provision for metering the liquids to be introduced, e.g. when adding syrups by weighing

Definitions

  • the present invention relates to a method of filling a container with a net weight of product at means of a filling member arranged to introduce the produced in the container while it is carried by a force sensor.
  • the simplest method is to have a container on a weighing member, the container itself being arranged below a filling member whose opening and closure are controlled by the weighing device according to the apparent weight that is measured by it.
  • the weight apparent not only includes the empty weight of the container and the net weight of the product contained in the container, but also the force that results from the jet of product on the surface of the product contained in the container.
  • This strength varies not only according to the opening of the organ filling but also depending on the viscosity of the product, so that if the viscosity of the product varies during filling, the measurement of weight made by the weighing device is distorted and the actual net weight of product introduced into the container at the end of filling does not equal the net weight of desired product.
  • the product between the filling member and the product surface in the container usually called drop tail
  • the weight of the fall tail varies in function of the diameter of the orifice of the filling member just before closing and the viscosity of the product.
  • jet pressure during the filling and the weight of the drop tail must therefore be compensated for eventually getting into the container the net weight of desired product.
  • the weighing member when introducing the container onto the organ of weighing and the establishment of the product stream during the flow control, the weighing member is subject to oscillations that distort the measurement of instantaneous flow and consequently the calculation of the total weight of product contained in the container.
  • To overcome this drawback is necessary to filter the signal of the weighing member, at least in the initial phase of filling, by complex algorithms that significantly increase the cost of implementation of this filling process.
  • An object of the present invention is to propose a method of filling a container that can be put into work with simple algorithms while allowing to obtain a great precision on the net weight of product introduced into the container.
  • the step of calculating an average flow of product minimizes the consequences of initial oscillations so that a precise result is achieved without it being necessary to use complex calculation algorithms.
  • a smoothed average flow rate is calculated by choosing moments of staggered readings relative to the flow control of sufficient way for the force sensor to be substantially stable over the time interval between moments of survey. The period of instability from cycle is thus automatically eliminated.
  • the initialization cycle implements substantially identical to those of the cycles set works later for the filling of others containers, so that the reference weight is determined without additional cost.
  • the method according to the invention is implemented by a device comprising in a manner known per se a feed member 1 connected to a filling member 2 disposed above a container 3 itself carried by a force sensor 4.
  • the feeding member is for example a tank carried by the platform rotation of a carousel or a separate tank of the carousel and connected to the platform by a pipe with a Turning joint. Flow from the organ feeding can be favored by a centrifugal pump.
  • the filling member 2 is for example a valve or a Archimedes screw controlled by a stepper motor, the speed of the motor determining the flow caused by the screw d'Archimpole, particularly in the case of a pasty product such as mayonnaise or a heterogeneous product such only a sauce with pieces.
  • the control of the filling member can not be performed directly on a debit value but on a physical parameter (opening section or speed of rotation of the screw), the actual flow not only dependent the physical parameter ordered but other parameters such that the density of the product, its viscosity and the pressure in the supply duct.
  • the device also comprises an organ time count 5 including a clock to give a common time base for the different bodies providing the implementation of the method according to the invention.
  • the diagram in Figure 1 illustrates the evolution of the force measured by the force sensor as a function of time while filling a one-liter bottle with milk.
  • the time of a filling cycle is the order of 5 seconds, which implies an average throughput of the order of 200 grams per second.
  • the establishment of the product jet therefore causes a shock on the bottom of the container, which explains the oscillations of the force measured by the force sensor for a little over a second from start of a cycle. It will be noted that these oscillations could be avoided if you expect a stabilization of the sensor force after the introduction of the container and if one performed flow control by increasing throughput in a very gradual way to avoid a shock on the force sensor.
  • Such a solution would, however, an extension of the duration of a filling cycle of totally incompatible with the rates of filling required at present.
  • a filling method comprising first an initialization cycle to acquire a number of parameters specific to the installation.
  • a container 3 is disposed on the force sensor 4 and a measurement of the empty weight of the container is carried out after allowing the force sensor to stabilize.
  • the measuring the empty weight of the container used for the cycle initialization is stored and will be subsequently denoted by reference empty weight.
  • a command of the flow is then triggered as well as a count of time to repeatedly measure a time flow of product from the flow control, the counting of time is for example performed at each thousandth of a second.
  • a measurement of the signal of strength provided by the force sensor is made to separate recording times, for example every 1 / 250th second. The force signal values thus recorded are used to calculate an average product flow in the time interval separating the times of the survey.
  • the average flow rate is calculated in two ways different: on the one hand a smoothed average flow calculated in choosing staggered reading instants in relation to the flow control enough so that the force sensor is substantially stable over the interval time separating the times of the survey.
  • the smoothed average flow rate will therefore not be calculated during the period of a little more than one second following the flow command but will be calculated repeatedly thereafter, for example between times T1, T2 and T3 which have been illustrated voluntarily very separately in Figure 1 for better understanding.
  • the smoothed average flow rate can be calculated either by taking the force difference between F2 and F3, or the force difference between F1 and F3 and by dividing this difference by the corresponding counted time.
  • F is representative of a force applied to the force sensor, i.e., not only the weight of the container and the net weight of product contained in the container, but also the force of the product jet
  • D1 is the smoothed average flow rate
  • t is the time taken from the flow control
  • B is the ordinate at the origin of the line representative of the smoothed average flow rate, that is to say that B is representative of the sum the empty weight T of the container and the force Fj of the product jet.
  • the force Fj is not directly measurable since it would suppose an instantaneous reaction of the force sensor at the time of the establishment of the jet.
  • a notional average rate Df is calculated by dividing the value of the force signal at a given instant by the time counted from the flow control.
  • the fictitious average rate is representative of a line joining the origin to the corresponding point of the filling curve.
  • Each calculation of the mean average rate corresponds to a different line.
  • a calculated evaluation of the time of filling from the average flow smoothed by dividing the net weight of product that one wishes to introduce into the container by the averaged smoothed flow calculated.
  • the weather counted since the flow command is periodically compared to the calculated filling time and a stop flow is controlled when the flow time of product is equal to the evaluation of the filling time.
  • the force sensor is then used in the same way a balance.
  • a reference weight Pr is then calculated subtracting from the desired net weight the difference between actual net weight and desired net weight. From the weight reference Pr can also be calculated a time of ref reference filling by dividing the weight of reference by the average flow smoothed during the cycle initializing.
  • the parameters of the initialization cycle are used according to the invention for subsequent filling cycles of the containers.
  • a container is arranged on the force sensor but unlike the cycle initialization a product flow control by the filling member is immediately performed without it is necessary to wait for a stabilization of the force sensor after the introduction of the container.
  • the flow control can even be anticipated compared at the introduction of the container on the force sensor so that despite the response time of the filling member, the jet of product reaches the container just when this one is set up on the force sensor, which allows to increase the rate of filling.
  • the value of the empty weight of the container as well obtained can be used to control net weight as will be indicated below.
  • a calculated evaluation of filling time is then performed by dividing the last weight of reference calculated by the last calculated average smooth flow.
  • a stop command of the product flow is performed when the product flow time counted by the time counting member 5 is equal to estimation of the filling time.
  • a comparison is made after each evaluation of filling time between the time of calculated fill and refill time calculated at the end of the initialization cycle and if the gap exceeds a critical value, for example 5% of the time of reference filling, the flow stop is ordered using reference refill time and an initialization cycle is started again in order to allow an update of the parameters of installation.
  • a critical value for example 5% of the time of reference filling
  • a control is preferably carried out at the end of each filling cycle.
  • This control consists of measuring the weight of the filled container, to compare the measured weight to a estimated weight equal to the sum of the estimated curb weight and net weight of desired product. When this control reveals between the measured weight and the estimated weight a gap exceeding a critical value, a new initialization cycle is sets off.
  • This control can also be used without replace the calculated evaluation of the filling time by reference refill time when the evaluation filling time deviates abnormally from the time reference filling.

Abstract

A method of filling a receptacle with a net weight substance by means of a filler member disposed to introduce the substance into the receptacle while the receptacle is being carried by a force sensor, the method comprising at least one cycle comprising the steps of:placing the receptacle on the force sensor;commanding the filler member to start a flow of the substance;repeatedly measuring the time for which the substance has been flowing since the start-of-flow command was issued;measuring a value of a signal supplied by the force sensor at least at first and second separate measurement instants;calculating a mean flow rate of the substance over the time interval between the measurement instants;making at least one computed evaluation of a filling time on the basis of the calculated mean flow rate and a reference weight; andcommanding the flow of substance to stop when the flow time of the substance is equal to the evaluated filling time.

Description

La présente invention concerne un procédé de remplissage d'un récipient avec un poids net de produit au moyen d'un organe de remplissage disposé pour introduire le produit dans le récipient alors que celui-ci est porté par un capteur de force.The present invention relates to a method of filling a container with a net weight of product at means of a filling member arranged to introduce the produced in the container while it is carried by a force sensor.

On connaít différents procédés de remplissage d'un récipient avec un poids net de produit. Traditionnellement, le procédé le plus simple consiste à disposer un récipient sur un organe de pesage, le récipient étant lui-même disposé en-dessous d'un organe de remplissage dont l'ouverture et la fermeture sont commandées par l'organe de pesage en fonction du poids apparent qui est mesuré par celui-ci. Le poids apparent comprend non seulement le poids à vide du récipient et le poids net de produit contenu dans le récipient, mais également la force qui résulte du jet de produit sur la surface du produit contenu dans le récipient. Cette force varie non seulement en fonction de l'ouverture de l'organe de remplissage mais également en fonction de la viscosité du produit, de sorte que si la viscosité du produit varie au cours du remplissage, la mesure de poids effectuée par l'organe de pesage est faussée et le poids net réel de produit introduit dans le récipient à la fin du remplissage n'est pas égal au poids net de produit souhaité.We know different filling processes of a container with a net weight of product. Traditionally, the simplest method is to have a container on a weighing member, the container itself being arranged below a filling member whose opening and closure are controlled by the weighing device according to the apparent weight that is measured by it. The weight apparent not only includes the empty weight of the container and the net weight of the product contained in the container, but also the force that results from the jet of product on the surface of the product contained in the container. This strength varies not only according to the opening of the organ filling but also depending on the viscosity of the product, so that if the viscosity of the product varies during filling, the measurement of weight made by the weighing device is distorted and the actual net weight of product introduced into the container at the end of filling does not equal the net weight of desired product.

En outre, au moment de la fermeture de l'organe de remplissage, le produit compris entre l'organe de remplissage et la surface de produit dans le récipient, généralement appelé queue de chute, vient augmenter le poids de produit finalement contenu dans le récipient à la fin du cycle de remplissage. Le poids de la queue de chute varie en fonction du diamètre de l'orifice de l'organe de remplissage juste avant la fermeture et de la viscosité du produit. Dans les procédés traditionnels, la pression du jet pendant le remplissage et le poids de la queue de chute doivent donc faire l'objet de compensations pour obtenir finalement dans le récipient le poids net de produit souhaité. In addition, at the time of the closure of the filling, the product between the filling member and the product surface in the container, usually called drop tail, just increase the weight product finally contained in the container at the end of filling cycle. The weight of the fall tail varies in function of the diameter of the orifice of the filling member just before closing and the viscosity of the product. In traditional processes, jet pressure during the filling and the weight of the drop tail must therefore be compensated for eventually getting into the container the net weight of desired product.

On connaít également du brevet français 2 679 516 un procédé de remplissage consistant à asservir le débit du produit sur un débit de référence et à effectuer le remplissage pendant un temps fixe prédéterminé calculé au préalable en divisant le poids net par le débit de référence. Ce procédé permet d'éliminer les effets de la pression du jet sur la surface du produit contenu dans le récipient en mesurant le débit instantané sur des intervalles de temps successifs pendant lesquels la force du jet de produit sur la surface du produit contenu dans le récipient est supposée constante. Ce procédé est théoriquement très satisfaisant mais en pratique l'asservissement du débit sur un débit de référence ne permet pas d'obtenir un débit réel exactement égal au débit de référence et il est donc nécessaire de procéder à des compensations en effectuant un contrôle du poids net réel après remplissage et en modifiant les paramètres de la boucle d'asservissement pour les cycles de remplissage ultérieurs afin que le poids net réel soit aussi proche que possible du poids net souhaité.We also know French patent 2,679,516 a filling process of slaving the flow of the produced on a reference flow and to perform the filling for a predetermined fixed time calculated in advance by dividing the net weight by the reference flow. This process eliminates the effects of jet pressure on the surface of the product contained in the container in measuring instantaneous flow over time intervals successive times during which the force of the product jet on the surface of the product contained in the container is assumed constant. This process is theoretically very satisfying but in practice the enslavement of the flow on a flow of reference does not allow to obtain a real flow exactly equal to the reference flow and it is therefore necessary to compensate by carrying out a control of the actual net weight after filling and by changing the servo loop parameters for the cycles of subsequent filling so that the actual net weight is also as close as possible to the desired net weight.

On connaít encore du document français 2 711 610 un procédé de remplissage comportant les étapes de mesurer sur des intervalles de temps successifs le débit instantané de produit introduit dans le récipient, calculer un poids total de produit introduit dans le récipient à partir du débit instantané sur chaque intervalle de temps, et commander un arrêt de l'écoulement de produit lorsque le poids total calculé atteint le poids net diminué de la queue de chute de produit. Ce procédé présente l'avantage de prendre en compte automatiquement les variations du débit instantané lors du calcul du poids total de produit contenu dans un récipient de sorte que le poids net réel de produit contenu dans le récipient après la fermeture de l'organe de remplissage n'est théoriquement affecté que par les variations de la queue de chute dont l'influence est faible. Toutefois, lors de l'introduction du récipient sur l'organe de pesage et de l'établissement du jet de produit lors de la commande d'écoulement, l'organe de pesage est soumis à des oscillations qui faussent la mesure du débit instantané et par voie de conséquence le calcul du poids total de produit contenu dans le récipient. Pour pallier cet inconvénient il est nécessaire de filtrer le signal de l'organe de pesage, au moins dans la phase initiale du remplissage, par des algorithmes complexes qui augmentent de façon importante le coût de mise en oeuvre de ce procédé de remplissage.We still know French document 2,711,610 a filling process comprising the steps of measuring over successive time intervals the instantaneous flow of product introduced into the container, calculate a weight total product introduced into the container from instantaneous flow over each time interval, and order a stop of the product flow when the total calculated weight reaches the net weight decreased by the tail of product drop. This method has the advantage of automatically take into account flow variations snapshot when calculating the total product weight in a container so the actual net product weight contained in the container after the closure of the organ of filling is only theoretically affected by the variations of the fall tail whose influence is weak. However, when introducing the container onto the organ of weighing and the establishment of the product stream during the flow control, the weighing member is subject to oscillations that distort the measurement of instantaneous flow and consequently the calculation of the total weight of product contained in the container. To overcome this drawback is necessary to filter the signal of the weighing member, at least in the initial phase of filling, by complex algorithms that significantly increase the cost of implementation of this filling process.

Un but de la présente invention est de proposer un procédé de remplissage d'un récipient qui puisse être mis en oeuvre avec des algorithmes simples tout en permettant d'obtenir une grande précision sur le poids net de produit introduit dans le récipient.An object of the present invention is to propose a method of filling a container that can be put into work with simple algorithms while allowing to obtain a great precision on the net weight of product introduced into the container.

En vue de la réalisation de ce but, on propose selon l'invention, un procédé de remplissage d'un récipient avec un produit au moyen d'un organe de remplissage disposé pour introduire le produit dans le récipient alors que celui-ci est porté par un capteur de force, ce procédé comprenant au moins un cycle comportant les étapes de :

  • disposer un récipient sur le capteur de force,
  • commander un écoulement de produit par l'organe de remplissage,
  • décompter de façon répétée un temps d'écoulement de produit depuis la commande d'écoulement,
  • mesurer à au moins un premier et un deuxième instants de relevé séparés une valeur d'un signal fourni par le capteur de force,
  • calculer un débit moyen de produit dans un intervalle de temps séparant les instants de relevé,
  • effectuer au moins une évaluation calculée d'un temps de remplissage à partir du débit moyen calculé et d'un poids de référence,
  • commander un arrêt de l'écoulement de produit lorsque le temps d'écoulement de produit est égal à l'évaluation du temps de remplissage.
With a view to achieving this object, the invention proposes a method of filling a container with a product by means of a filling member arranged to introduce the product into the container while it is being carried. by a force sensor, this method comprising at least one cycle comprising the steps of:
  • have a container on the force sensor,
  • controlling a flow of product through the filling member,
  • repeatedly counting a product flow time from the flow control,
  • measuring at least a first and a second separate measurement times a value of a signal supplied by the force sensor,
  • calculate an average product flow in a time interval separating the recording times,
  • perform at least one calculated evaluation of a filling time from the calculated average flow rate and a reference weight,
  • controlling a stop of the product flow when the product flow time is equal to the evaluation of the filling time.

Ainsi, l'étape de calcul d'un débit moyen de produit minimise les conséquences des oscillations de départ de sorte qu'un résultat précis est obtenu sans qu'il soit nécessaire d'utiliser des algorithmes de calcul complexes.Thus, the step of calculating an average flow of product minimizes the consequences of initial oscillations so that a precise result is achieved without it being necessary to use complex calculation algorithms.

Selon une version avantageuse de l'invention, un débit moyen lissé est calculé en choisissant des instants de relevé décalés par rapport à la commande d'écoulement de façon suffisante pour que le capteur de force soit sensiblement stable sur l'intervalle de temps séparant les instants de relevé. La période d'instabilité de départ du cycle est ainsi automatiquement éliminée.According to an advantageous version of the invention, a smoothed average flow rate is calculated by choosing moments of staggered readings relative to the flow control of sufficient way for the force sensor to be substantially stable over the time interval between moments of survey. The period of instability from cycle is thus automatically eliminated.

Selon un mode de mise en oeuvre préféré de l'invention, le procédé comporte un cycle d'initialisation comportant les étapes de :

  • disposer un récipient d'initialisation sur le capteur de force,
  • de préférence, mesurer un poids à vide de référence du récipient au moyen du capteur de force et mémoriser le poids à vide de référence,
  • commander un écoulement de produit par l'organe de remplissage,
  • décompter de façon répétée un temps d'écoulement de produit depuis la commande d'écoulement,
  • calculer au moins une fois le débit moyen lissé de produit,
  • effectuer au moins une évaluation calculée d'un temps de remplissage à partir du débit moyen lissé et d'un poids net de produit souhaité,
  • commander un arrêt de l'écoulement de produit lorsque le temps d'écoulement de produit est égal à l'évaluation du temps de remplissage,
  • mesurer le poids du récipient après remplissage et en déduire une différence entre le poids net de produit souhaité et un poids net réel de produit dans le récipient,
  • calculer le poids de référence en déduisant du poids net souhaité la différence entre le poids net souhaité et le poids net réel.
According to a preferred embodiment of the invention, the method comprises an initialization cycle comprising the steps of:
  • have an initialization container on the force sensor,
  • preferably, measuring a reference empty weight of the container by means of the force sensor and storing the reference empty weight,
  • controlling a flow of product through the filling member,
  • repeatedly counting a product flow time from the flow control,
  • calculate at least once the smoothed product flow rate,
  • perform at least one calculated evaluation of a filling time from the smoothed average flow rate and a desired net product weight,
  • controlling a stop of the product flow when the product flow time is equal to the evaluation of the filling time,
  • measuring the weight of the container after filling and deducting a difference between the net weight of desired product and a net actual product weight in the container,
  • calculate the reference weight by deducting from the desired net weight the difference between the desired net weight and the actual net weight.

Ainsi, le cycle d'initialisation met en oeuvre des étapes sensiblement identiques à celles des cycles mis en oeuvre ultérieurement pour le remplissage des autres récipients, de sorte que le poids de référence est déterminé sans coût supplémentaire.Thus, the initialization cycle implements substantially identical to those of the cycles set works later for the filling of others containers, so that the reference weight is determined without additional cost.

D'autres particularités et avantages de l'invention apparaítront à la lecture de la description qui suit d'un mode de mise en oeuvre préféré du procédé selon l'invention en référence aux figues ci-jointes parmi lesquelles :

  • la figure 1 est un diagramme illustrant l'évolution de la force mesurée par le capteur de force en fonction du temps pendant un cycle de remplissage,
  • la figure 2 est une représentation schématique par blocs des étapes de remplissage pendant un cycle d'initialisation selon le mode de mise en oeuvre préféré de l'invention,
  • la figure 3 est une représentation schématique par blocs des étapes de remplissage pendant un cycle de remplissage normal selon un mode de mise en oeuvre préféré de l'invention.
Other features and advantages of the invention will appear on reading the following description of a preferred embodiment of the method according to the invention with reference to the attached figs, among which:
  • FIG. 1 is a diagram illustrating the evolution of the force measured by the force sensor as a function of time during a filling cycle,
  • FIG. 2 is a schematic block representation of the filling steps during an initialization cycle according to the preferred embodiment of the invention,
  • Figure 3 is a schematic block diagram of the filling steps during a normal fill cycle according to a preferred embodiment of the invention.

En référence à la figure 2, le procédé selon l'invention est mis en oeuvre par un dispositif comportant d'une façon connue en soi un organe d'alimentation 1 relié à un organe de remplissage 2 disposé au-dessus d'un récipient 3 lui-même porté par un capteur de force 4. L'organe d'alimentation est par exemple une cuve portée par la plate-forme rotative d'un carrousel ou une cuve séparée du carrousel et reliée à la plate-forme par une canalisation comportant un joint tournant. L'écoulement à partir de l'organe d'alimentation peut être favorisé par une pompe centrifuge. L'organe de remplissage 2 est par exemple une vanne ou une vis d'Archimède commandée par un moteur pas à pas, la vitesse du moteur déterminant le débit entraíné par la vis d'Archimède, en particulier dans le cas d'un produit pâteux tel que de la mayonnaise ou d'un produit hétérogène tel qu'une sauce avec des morceaux. On remarquera à ce propos que la commande de l'organe de remplissage ne peut pas être effectuée directement sur une valeur de débit mais sur un paramètre physique (section d'ouverture ou vitesse de rotation de la vis), le débit réel dépendant non seulement du paramètre physique commandé mais d'autres paramètres tels que la densité du produit, sa viscosité et la pression dans le conduit d'alimentation.With reference to FIG. 2, the method according to the invention is implemented by a device comprising in a manner known per se a feed member 1 connected to a filling member 2 disposed above a container 3 itself carried by a force sensor 4. The feeding member is for example a tank carried by the platform rotation of a carousel or a separate tank of the carousel and connected to the platform by a pipe with a Turning joint. Flow from the organ feeding can be favored by a centrifugal pump. The filling member 2 is for example a valve or a Archimedes screw controlled by a stepper motor, the speed of the motor determining the flow caused by the screw d'Archimède, particularly in the case of a pasty product such as mayonnaise or a heterogeneous product such only a sauce with pieces. We will notice in this regard that the control of the filling member can not be performed directly on a debit value but on a physical parameter (opening section or speed of rotation of the screw), the actual flow not only dependent the physical parameter ordered but other parameters such that the density of the product, its viscosity and the pressure in the supply duct.

Le dispositif comporte également un organe de décompte de temps 5 comprenant une horloge destinée à donner une base de temps commune aux différents organes assurant la mise en oeuvre du procédé selon l'invention.The device also comprises an organ time count 5 including a clock to give a common time base for the different bodies providing the implementation of the method according to the invention.

Le diagramme de la figure 1 illustre l'évolution de la force mesurée par le capteur de force en fonction du temps pendant le remplissage d'une bouteille de un litre avec du lait. Le temps d'un cycle de remplissage est de l'ordre de 5 secondes, ce qui implique un débit moyen de l'ordre de 200 grammes par seconde. On imagine aisément qu'un débit aussi élevé implique une force de jet importante. L'établissement du jet de produit provoque donc un choc sur le fond du récipient, ce qui explique les oscillations de la force mesurée par le capteur.de force pendant un peu plus d'une seconde à partir du démarrage d'un cycle. On remarquera que ces oscillations pourraient être évitées si l'on attendait une stabilisation du capteur de force après l'introduction du récipient et si l'on effectuait une commande d'écoulement en augmentant le débit de façon très progressive pour éviter un choc sur le capteur de force. Une telle solution entraínerait toutefois un allongement de la durée d'un cycle de remplissage de façon totalement incompatible avec les cadences de remplissage exigées à l'heure actuelle. The diagram in Figure 1 illustrates the evolution of the force measured by the force sensor as a function of time while filling a one-liter bottle with milk. The time of a filling cycle is the order of 5 seconds, which implies an average throughput of the order of 200 grams per second. We imagine easily that such a high flow implies a jet force important. The establishment of the product jet therefore causes a shock on the bottom of the container, which explains the oscillations of the force measured by the force sensor for a little over a second from start of a cycle. It will be noted that these oscillations could be avoided if you expect a stabilization of the sensor force after the introduction of the container and if one performed flow control by increasing throughput in a very gradual way to avoid a shock on the force sensor. Such a solution would, however, an extension of the duration of a filling cycle of totally incompatible with the rates of filling required at present.

Selon le mode de mise en oeuvre préféré de l'invention, on prévoit un procédé de remplissage comprenant tout d'abord un cycle d'initialisation permettant d'acquérir un certain nombre de paramètres propres à l'installation. Pendant le cycle d'initialisation, un récipient 3 est disposé sur le capteur de force 4 et une mesure du poids à vide du récipient est effectuée après avoir laissé le capteur de force se stabiliser. La mesure du poids à vide du récipient utilisé pour le cycle d'initialisation est mémorisée et sera par la suite désignée par poids à vide de référence. Une commande de l'écoulement est ensuite déclenchée ainsi qu'un décompte de temps permettant de mesurer de façon répétée un temps d'écoulement de produit depuis la commande d'écoulement, le décompte de temps est par exemple effectué à chaque millième de seconde. Parallèlement, une mesure du signal de force fournie par le capteur de force est effectués à des instants de relevé séparés, par exemple tous les 1/250ème de seconde. Les valeurs du signal de force ainsi relevées sont utilisées pour calculer un débit moyen de produit dans l'intervalle de temps séparant les instants de relevé.According to the preferred embodiment of the invention provides a filling method comprising first an initialization cycle to acquire a number of parameters specific to the installation. During the initialization cycle, a container 3 is disposed on the force sensor 4 and a measurement of the empty weight of the container is carried out after allowing the force sensor to stabilize. The measuring the empty weight of the container used for the cycle initialization is stored and will be subsequently denoted by reference empty weight. A command of the flow is then triggered as well as a count of time to repeatedly measure a time flow of product from the flow control, the counting of time is for example performed at each thousandth of a second. In parallel, a measurement of the signal of strength provided by the force sensor is made to separate recording times, for example every 1 / 250th second. The force signal values thus recorded are used to calculate an average product flow in the time interval separating the times of the survey.

Selon le mode de mise en oeuvre préféré de l'invention, le débit moyen est calculé de deux façons différentes : d'une part un débit moyen lissé calculé en choisissant des instants de relevé décalés par rapport à la commande d'écoulement de façon suffisante pour que le capteur de force soit sensiblement stable sur l'intervalle de temps séparant les instants de relevé.According to the preferred embodiment of the invention, the average flow rate is calculated in two ways different: on the one hand a smoothed average flow calculated in choosing staggered reading instants in relation to the flow control enough so that the force sensor is substantially stable over the interval time separating the times of the survey.

En référence à la figure 1, le débit moyen lissé ne sera donc pas calculé pendant la période d'un peu plus d'une seconde qui suit la commande d'écoulement mais sera calculé de façon répétée par la suite, par exemple entre des instants T1, T2 et T3 qui ont été illustrés de façon volontairement très séparée sur la figure 1 pour une meilleure compréhension. Le débit moyen lissé est calculé en divisant un écart de force entre deux instants de relevé par le temps décompté entre ces deux instants. Si l'on désigne par F1 la valeur de la force mesurée à l'instant t1, F2 la force mesurée à l'instant t2..., on peut donc calculer un premier débit moyen lissé entre des instants t1 et t2 selon la formule D1 = (F2 - F1)/(t2 - t1). With reference to FIG. 1, the smoothed average flow rate will therefore not be calculated during the period of a little more than one second following the flow command but will be calculated repeatedly thereafter, for example between times T1, T2 and T3 which have been illustrated voluntarily very separately in Figure 1 for better understanding. The smoothed average flow rate is calculated by dividing a force difference between two times of reading by the time counted between these two instants. If we denote by F1 the value of the force measured at time t1, F2 the force measured at time t2 ..., we can calculate a first average flow smoothed between instants t1 and t2 according to the formula D1 = (F2 - F1) / (t2 - t1).

A l'instant t3 ultérieur, le débit moyen lissé peut être calculé soit en prenant l'écart de force entre F2 et F3, soit l'écart de force entre F1 et F3 et en divisant cet écart par le temps décompté correspondant. Afin d'obtenir un meilleur lissage, on peut également calculer le débit moyen lissé en effectuant une moyenne de la force relevée à différents instants précédant l'instant de relevé et en effectuant le calcul de l'écart de force entre la valeur relevée au dernier instant et la moyenne calculée sur les instants précédents, puis en divisant par l'intervalle de temps pris entre le dernier instant de relevé et la moyenne des instants de relevé pris en compte pour le calcul de la moyenne des écarts de force. On peut également effectuer un lissage en effectuant une moyenne de plusieurs débits moyens lissés. Quoi qu'il en soit, chaque débit moyen lissé calculé est caractéristique d'une droite d'équation F = D1.t+B où F est représentatif d'une force appliquée sur le capteur de force, c'est-à-dire non seulement le poids du récipient et le poids net de produit contenu dans le récipient, mais également la force du jet de produit, D1 est le débit moyen lissé, t est le temps décompté depuis la commande d'écoulement, et B est l'ordonnée à l'origine de la droite représentative du débit moyen lissé, c'est-à-dire que B est représentatif de la somme du poids à vide T du récipient et de la force Fj du jet de produit. On remarquera que la force Fj n'est pas directement mesurable car elle supposerait une réaction instantanée du capteur de force au moment de l'établissement du jet.At the subsequent time t3, the smoothed average flow rate can be calculated either by taking the force difference between F2 and F3, or the force difference between F1 and F3 and by dividing this difference by the corresponding counted time. In order to obtain a better smoothing, it is also possible to calculate the smoothed average flow rate by averaging the force measured at different times preceding the time of recording and by calculating the difference in force between the value recorded at the last moment and the average calculated on the previous instants, then dividing by the interval of time taken between the last moment of reading and the average of the instants of statement taken into account for the calculation of the average of the deviations of force. Smoothing can also be performed by averaging several smoothed average flows. Anyway, each calculated smoothed average flow is characteristic of an equation line F = D1.t + B where F is representative of a force applied to the force sensor, i.e., not only the weight of the container and the net weight of product contained in the container, but also the force of the product jet, D1 is the smoothed average flow rate, t is the time taken from the flow control, and B is the ordinate at the origin of the line representative of the smoothed average flow rate, that is to say that B is representative of the sum the empty weight T of the container and the force Fj of the product jet. It will be noted that the force Fj is not directly measurable since it would suppose an instantaneous reaction of the force sensor at the time of the establishment of the jet.

Par ailleurs, un débit moyen fictif Df est calculé en divisant la valeur du signal de force à un instant donné par le temps décompté depuis la commande d'écoulement. Le débit moyen fictif est représentatif d'une droite joignant l'origine au point correspondant de la courbe de remplissage. A chaque calcul du débit moyen fictif correspond une droite différente. Afin de ne pas surcharger la figure, seules les droites représentatives des débits moyens fictifs à l'instant T2 et à la fin du remplissage ont été représentées sur la figure 1. La droite représentative du débit moyen fictif a pour équation F = Df.t. Furthermore, a notional average rate Df is calculated by dividing the value of the force signal at a given instant by the time counted from the flow control. The fictitious average rate is representative of a line joining the origin to the corresponding point of the filling curve. Each calculation of the mean average rate corresponds to a different line. In order not to overload the figure, only the straight lines representative of the imaginary mean flow rates at the instant T2 and at the end of the filling have been represented in FIG. 1. The line representative of the imaginary average flow rate has for equation F = Df.t.

Lorsque le débit moyen lissé et le débit moyen fictif sont calculés à un même instant de relevé la force mesurée par le capteur de force est la même, il est donc possible de calculer l'ordonnée à l'origine de la droite représentative du débit lissé par l'intersection des droites, soit Df.t = D1.t + B d'où l'on tire B = (Df - D1)/t. When the smoothed mean flow rate and the mean average flow rate are calculated at the same time of reading, the force measured by the force sensor is the same, it is therefore possible to calculate the ordinate at the origin of the straight line representative of the smoothed flow rate. by the intersection of the lines, either Df.t = D1.t + B from where we draw B = (Df - D1) / t.

Pendant le cycle d'initialisation, le poids à vide de référence Tr du récipient est connu. Il est donc possible de calculer une force de jet de référence Fjr par application de la formule Fjr = Br - Tr où Br est l'ordonnée à l'origine de la droite représentative du débit moyen lissé pendant le cycle d'initialisation.During the initialization cycle, the reference empty weight Tr of the container is known. It is therefore possible to calculate a reference jet force Fjr by applying the formula Fjr = Br - Tr where Br is the ordinate at the origin of the straight line representative of the average flow smoothed during the initialization cycle.

Simultanément au calcul de la force de jet de référence, on effectue une évaluation calculée du temps de remplissage à partir du débit moyen lissé en divisant le poids net de produit que l'on souhaite introduire dans le récipient par le débit moyen lissé calculé. Le temps décompté depuis la commande d'écoulement est périodiquement comparé au temps de remplissage ainsi calculé et un arrêt de l'écoulement est commandé lorsque le temps d'écoulement de produit est égal à l'évaluation du temps de remplissage.Simultaneously with the calculation of the jet force of reference, a calculated evaluation of the time of filling from the average flow smoothed by dividing the net weight of product that one wishes to introduce into the container by the averaged smoothed flow calculated. The weather counted since the flow command is periodically compared to the calculated filling time and a stop flow is controlled when the flow time of product is equal to the evaluation of the filling time.

On remarquera qu'en raison de l'assimilation qui a été faite de la courbe de remplissage à une droite et en raison du fait que le poids de la queue de chute n'a pas été pris en compte pour commander l'arrêt de l'écoulement, le poids net réel de produit contenu dans le récipient à la fin du cycle d'initialisation ne peut pas être égal au poids net souhaité.It should be noted that because of the assimilation was made of the filling curve to a straight and in because of the fact that the weight of the drop tail does not have been taken into account to control the flow stop, the actual net weight of the product contained in the container at the end of the initialization cycle can not be equal to desired net weight.

Selon une caractéristique de l'invention on effectue dans le cycle d'initialisation une mesure du poids total après remplissage et un calcul du poids net réel par soustraction du poids à vide de référence Tr préalablement mémorisé, le capteur de force est alors utilisé à la façon d'une balance. Un poids de référence Pr est ensuite calculé en soustrayant du poids net souhaité la différence entre le poids net réel et le poids net souhaité. A partir du poids de référence Pr on peut également calculer un temps de remplissage de référence tr en divisant le poids de référence par le débit moyen lissé au cours du cycle d'initialisation.According to one characteristic of the invention perform a weight measurement in the initialization cycle total after filling and a calculation of the actual net weight per subtraction of the reference empty weight Tr previously memorized, the force sensor is then used in the same way a balance. A reference weight Pr is then calculated subtracting from the desired net weight the difference between actual net weight and desired net weight. From the weight reference Pr can also be calculated a time of ref reference filling by dividing the weight of reference by the average flow smoothed during the cycle initializing.

En référence à la figure 3, les paramètres du cycle d'initialisation sont utilisés selon l'invention pour les cycles de remplissage ultérieurs des récipients. Pour chaque cycle de remplissage un récipient est disposé sur le capteur de force mais contrairement au cycle d'initialisation une commande d'écoulement de produit par l'organe de remplissage est immédiatement effectuée sans qu'il soit nécessaire d'attendre une stabilisation du capteur de force après l'introduction du récipient. La commande d'écoulement peut même être anticipée par rapport à l'introduction du récipient sur le capteur de force afin qu'en dépit du temps de réponse de l'organe de remplissage, le jet de produit atteigne le récipient au moment même où celui-ci est mis en place sur le capteur de force, ce qui permet d'augmenter la cadence de remplissage. De la même façon que pendant le cycle d'initialisation un calcul du débit moyen lissé et du débit moyen fictif est effectuée de façon répétée à différents instants de relevé, ce qui permet à chaque fois de déterminer l'ordonnée à l'origine de la droite représentative du débit moyen lissé comme dans le cycle d'initialisation.With reference to Figure 3, the parameters of the initialization cycle are used according to the invention for subsequent filling cycles of the containers. For each filling cycle a container is arranged on the force sensor but unlike the cycle initialization a product flow control by the filling member is immediately performed without it is necessary to wait for a stabilization of the force sensor after the introduction of the container. The flow control can even be anticipated compared at the introduction of the container on the force sensor so that despite the response time of the filling member, the jet of product reaches the container just when this one is set up on the force sensor, which allows to increase the rate of filling. Of the same way that during the initialization cycle a calculation of the smoothed average flow rate and mean fictitious average flow is performed from repeatedly at different times of recording, which allows each time to determine the y-intercept of the right representative of the average flow smoothed as in the initialization cycle.

La valeur calculée de cette ordonnée à l'origine est cette fois utilisée pour effectuer une estimation du poids à vide T du récipient en cours de remplissage en utilisant la force de jet de référence préalablement mémorisée par application de la formule T = B - Fjr. The calculated value of this ordinate at the origin is this time used to make an estimate of the empty weight T of the container being filled using the reference jet force previously stored by applying the formula T = B - Fjr.

La valeur du poids à vide du récipient ainsi obtenue peut être utilisée pour contrôler le poids net ainsi qu'il sera indiqué ci-dessous.The value of the empty weight of the container as well obtained can be used to control net weight as will be indicated below.

Une évaluation calculée de temps de remplissage est ensuite effectuée en divisant le dernier poids de référence calculé par le dernier débit moyen lissé calculé.A calculated evaluation of filling time is then performed by dividing the last weight of reference calculated by the last calculated average smooth flow.

Une commande d'arrêt de l'écoulement de produit est effectuée lorsque le temps d'écoulement de produit décompté par l'organe de décompte de temps 5 est égal à l'estimation du temps de remplissage.A stop command of the product flow is performed when the product flow time counted by the time counting member 5 is equal to estimation of the filling time.

Selon le mode de mise en oeuvre préféré illustré par la figure 3, une comparaison est effectuée après chaque évaluation de temps de remplissage entre le temps de remplissage calculé et le temps de remplissage de référence calculé à la fin du cycle d'initialisation et si l'écart dépasse une valeur critique, par exemple 5 % du temps de remplissage de référence, l'arrêt de l'écoulement est commandé en utilisant le temps de remplissage de référence et un cycle d'initialisation est à nouveau lancé afin de permettre une remise à jour des paramètres de l'installation.According to the preferred embodiment illustrated in Figure 3, a comparison is made after each evaluation of filling time between the time of calculated fill and refill time calculated at the end of the initialization cycle and if the gap exceeds a critical value, for example 5% of the time of reference filling, the flow stop is ordered using reference refill time and an initialization cycle is started again in order to allow an update of the parameters of installation.

Si le temps du cycle de remplissage est suffisamment court par rapport à la cadence souhaitée, un contrôle est de préférence effectué à la fin de chaque cycle de remplissage. Ce contrôle consiste à mesurer le poids du récipient rempli, à comparer le poids mesuré à un poids estimé égal à la somme du poids à vide estimé et du poids net de produit souhaité. Lorsque ce contrôle révèle entre le poids mesuré et le poids estimé un écart dépassant une valeur critique, un nouveau cycle d'initialisation est déclenché. Ce contrôle peut également être utilisé sans remplacer l'évaluation calculée du temps de remplissage par le temps de remplissage de référence lorsque l'évaluation du temps de remplissage s'écarte de façon anormale du temps de remplissage de référence.If the time of the filling cycle is sufficiently short compared to the desired rate, a control is preferably carried out at the end of each filling cycle. This control consists of measuring the weight of the filled container, to compare the measured weight to a estimated weight equal to the sum of the estimated curb weight and net weight of desired product. When this control reveals between the measured weight and the estimated weight a gap exceeding a critical value, a new initialization cycle is sets off. This control can also be used without replace the calculated evaluation of the filling time by reference refill time when the evaluation filling time deviates abnormally from the time reference filling.

Bien entendu, l'invention n'est pas limitée au mode de mise en oeuvre décrit et est susceptible de variantes sans sortir du cadre de l'invention tel que défini par les revendications.Of course, the invention is not limited to mode of implementation described and is likely to variants without departing from the scope of the invention as defined by the claims.

En particulier, bien que l'acquisition des paramètres de l'installation ait été décrite en mettant en oeuvre un cycle d'initialisation, on peut prévoir d'obtenir ces paramètres soit par des calculs, soit par des mesures effectuées indépendamment de la mise en oeuvre du procédé de remplissage selon l'invention. Par exemple, lorsque les récipients ont un poids à vide constant d'un récipient à un autre, on peut supprimer l'étape de mesure du poids à vide du récipient dans le cycle d'initialisation ainsi que l'étape d'estimation du poids à vide du récipient dans les cycles de remplissage ultérieurs.In particular, although the acquisition of The parameters of the installation have been described by an initialization cycle, we can expect to obtain these parameters either by calculations or by measurements carried out independently of the implementation of the process filling according to the invention. For example, when containers have a constant curb weight of a container to a other, we can remove the step of measuring the empty weight of the container in the initialization cycle as well as the step of estimating the empty weight of the container in the subsequent filling cycles.

Lorsque les paramètres de l'installation sont très constants ou lorsque les contraintes de précision du remplissage sont réduites, on peut également prévoir de simplifier le procédé selon l'invention en effectuant une évaluation calculée du temps de remplissage à partir d'un seul calcul du débit moyen, par exemple environ quatre secondes après la commande d'écoulement.When the settings of the installation are very constant or when the precision constraints of the filling is reduced, it is also possible to simplify the process according to the invention by carrying out a calculated evaluation of the filling time from a only calculation of the average flow, for example about four seconds after the flow control.

Par ailleurs, on remarquera sur la figure 1 qu'en raison de la forte pente de la courbe de remplissage dans sa partie sensiblement rectiligne et du faible décalage de l'ordonnée à l'origine, la droite représentative du débit moyen fictif est très proche de la courbe de remplissage réel en particulier en fin de remplissage. Sans sortir du cadre de l'invention, on peut donc prévoir d'effectuer l'estimation de temps de remplissage en remplaçant le débit moyen lissé par le débit moyen fictif et d'effectuer une correction soit par des mesures effectuées lors d'un cycle d'initialisation, soit par des corrections calculées.Moreover, we can see in Figure 1 that because of the steep slope of the filling curve in its substantially rectilinear part and the small offset of the ordinate at the origin, the line representative of the flow fictitious medium is very close to the filling curve real especially at the end of filling. Without leaving the framework of the invention, it is therefore possible to provide estimating filling time by replacing flow medium smoothed by the average fictitious throughput and perform a correction either by measurements made during a cycle initialization, or by calculated corrections.

Dans le cas d'une comparaison entre le temps de remplissage évalué et un temps de remplissage de référence, on peut prévoir une mise à jour du temps de remplissage de référence en remplaçant le temps de remplissage de référence initial par le dernier temps de référence de remplissage évalué lorsque l'écart ne dépasse pas la valeur critique. On peut également prévoir un deuxième seuil critique pour lequel une alarme est immédiatement déclenchée lorsque l'écart entre le temps de remplissage évalué et le temps de remplissage de référence dépasse ce second seuil.In the case of a comparison between the time of rated fill and reference refill time, it is possible to update the filling time of reference by replacing the filling time of initial reference by the last reference time of filling evaluated when the difference does not exceed the value critical. We can also provide a second threshold critical for which an alarm is immediately triggered when the gap between the filling time evaluated and the reference refill time exceeds this second threshold.

Claims (7)

  1. A method of filling a receptacle with a net weight substance by means of a filler member disposed to introduce the substance into the receptacle while the receptacle is being carried by a force sensor, the method being characterized in that it comprises at least one cycle comprising the steps of:
    placing the receptacle on the force sensor;
    commanding the filler member to start a flow of the substance;
    repeatedly measuring the time for which the substance has been flowing since the start-of-flow command was issued;
    measuring a value of a signal supplied by the force sensor at least at first and second separate measurement instants;
    calculating a mean flow rate of the substance over the time interval between the measurement instants;
    making at least one computed evaluation of a filling time on the basis of the calculated mean flow rate and a reference weight; and
    commanding the flow of substance to stop when the flow time of the substance is equal to the evaluated filling time.
  2. A method according to claim 1, characterized in that a smoothed mean flow rate is calculated by selecting measurement instants that are offset from the start-of-flow command sufficiently for the force sensor to be substantially stable over the time interval between the measurement instants.
  3. A method according to claim 2, characterized in that it includes an initialization cycle comprising the steps of:
    placing a receptacle on the force sensor;
    commanding the filler member to start the flow of substance;
    repeatedly measuring a substance flow time from the start-of-flow command;
    calculating at least once the smoothed mean flow rate of the substance;
    calculating at least one evaluation of a filling time on the basis of the smoothed mean flow rate and a desired net weight of substance;
    commanding the flow of substance to stop when the product flow time is equal to the evaluated filling time;
    measuring the weight of the receptacle after filling and deducing therefrom a difference between the desired net weight of substance and the real net weight of substance in the receptacle; and
    calculating the reference weight by subtracting the difference between the desired net weight and the real net weight from the desired net weight.
  4. A method according to claim 3, characterized in that it includes a prior step of measuring a reference tare weight of the receptacle by means of the force sensor, and storing the reference tare weight.
  5. A method according to claim 3, characterized in that during the initialization cycle, it includes the steps of:
    calculating at least once a simplified mean flow rate between the start-of-flow command and a latest measurement instant;
    calculating the difference between the simplified mean flow rate and the smoothed mean flow rate by reference to a reference tare weight of the receptacle; and
    deducing therefrom a reference jet force of the product and storing it;
       and in that, during each subsequent cycle, it includes the steps of:
    calculating at least once the simplified mean flow rate; and
    calculating the difference between the simplified mean flow rate and the smoothed mean flow rate with reference to the reference jet force and estimating an tare weight for the receptacle that is being filled.
  6. A method according to claim 5, characterized in that it includes the steps of measuring the weight of the receptacle, comparing the measured weight with an estimated weight equal to the sum of the estimated tare weight plus the desired net weight of substance, and triggering a new initialization cycle whenever the difference between the measured weight and the estimated weight exceeds a critical value.
  7. A method according to claim 6, characterized in that during the initialization cycle it includes, after correcting the reference weight, the steps of evaluating a reference filling time and of storing it, and in that during each subsequent cycle, it includes the steps of comparing the evaluated filling time for the receptacle being filled with the reference filling time and of comparing the measured weight and the estimated weight when a difference between the estimated filling time and the reference filling time exceeds a critical value.
EP00949609A 1999-07-19 2000-07-03 Method for filling a container Expired - Lifetime EP1196346B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DK00949609T DK1196346T3 (en) 1999-07-19 2000-07-03 Method of filling a container

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR9909327 1999-07-19
FR9909327A FR2797258B1 (en) 1999-07-19 1999-07-19 METHOD FOR FILLING A CONTAINER
PCT/FR2000/001882 WO2001005698A1 (en) 1999-07-19 2000-07-03 Method for filling a container

Publications (2)

Publication Number Publication Date
EP1196346A1 EP1196346A1 (en) 2002-04-17
EP1196346B1 true EP1196346B1 (en) 2004-09-15

Family

ID=9548245

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00949609A Expired - Lifetime EP1196346B1 (en) 1999-07-19 2000-07-03 Method for filling a container

Country Status (11)

Country Link
US (1) US6334471B1 (en)
EP (1) EP1196346B1 (en)
JP (1) JP2003505674A (en)
AT (1) ATE276196T1 (en)
BR (1) BR0012587A (en)
DE (1) DE60013835T2 (en)
DK (1) DK1196346T3 (en)
ES (1) ES2226889T3 (en)
FR (1) FR2797258B1 (en)
PT (1) PT1196346E (en)
WO (1) WO2001005698A1 (en)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6644344B2 (en) * 2001-05-11 2003-11-11 Ashland, Inc. Method and apparatus for metering a flow rate of a fluid
DE10209435C1 (en) * 2002-03-05 2003-08-14 Feige Abfuelltechnik Filling device for simultaneous filling of several containers has residual weight difference values for all containers used for calculating valve openings for corresponding filling valves
DE10307672A1 (en) * 2003-02-21 2004-09-09 Krohne Meßtechnik GmbH & Co KG Process for filling a liquid or pourable medium into a container
US6779569B1 (en) * 2003-12-18 2004-08-24 The United States Of America As Represented By The Secretary Of The Navy Liquid filling control method for multiple tanks
US7527078B2 (en) * 2005-10-13 2009-05-05 Fluid Management, Llc Apparatuses for dispensing materials volumetrically and gravimetrically based on a stored formula and methods of dispensing formulas using the same
AU2007302610B2 (en) * 2006-09-26 2014-04-10 Autopour Pty Ltd Dispensing apparatus and weighing process with control unit
EP1947427A1 (en) * 2007-01-19 2008-07-23 Mettler-Toledo AG Method for optimising dosage processes and dosage device
DE102007042433A1 (en) * 2007-09-06 2009-03-12 Iwk Verpackungstechnik Gmbh Method and device for filling tubes in a tube filling machine
JP5040027B2 (en) * 2007-11-09 2012-10-03 日立アロカメディカル株式会社 Liquid medicine dispensing device
EP2208679B1 (en) 2007-11-09 2015-04-15 Hitachi Aloka Medical, Ltd. Liquid medicine dispensing device
DE102008016846A1 (en) * 2008-04-01 2009-10-15 Khs Ag Method and device for filling in particular large-volume containers
US8424572B2 (en) 2009-09-23 2013-04-23 The Procter & Gamble Company Method for controlling the transfer of materials
DE102010004068B9 (en) 2010-01-05 2021-04-22 Fischbach Kg Kunststoff-Technik Method and filling device for filling a cartridge with at least one material
EP2372321B1 (en) * 2010-02-24 2012-11-07 Mettler-Toledo AG Method and device for filling target containers
CN103786933B (en) * 2012-10-29 2016-05-18 中国石油化工股份有限公司 The online SPC analytical system of Weighing type bulking equipment metering process ability and method
DE102013110108A1 (en) * 2013-09-13 2015-03-19 Khs Gmbh Printing system for printing on bottles or similar containers and printing device or machine with such a printing system
CN104944341A (en) * 2015-06-24 2015-09-30 安丘市鼎正机械设备有限公司 Non-contact filling device for filling machine
JP7011882B2 (en) * 2018-01-24 2022-01-27 株式会社エー・アンド・デイ Weighing device with flow meter function
DE102018133121A1 (en) * 2018-12-20 2020-06-25 Krones Ag Device for filling containers and method for operating the device
US11698285B2 (en) * 2020-01-02 2023-07-11 Kyndryl, Inc. Monitoring dispensation of a substance

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4526215A (en) * 1983-07-14 1985-07-02 Harrison William J Apparatus for forming mixtures of fluids
ES2037532T3 (en) 1989-06-27 1993-06-16 Group S.E.R.A.C. DEVICE FOR FILLING PONDERAL DOSAGE CONTAINERS.
FR2679516B1 (en) * 1991-07-23 1993-11-12 Andre Graffin WEIGHT DOSING METHOD AND DEVICE FOR FILLING CONTAINERS.
DE9306625U1 (en) * 1993-05-03 1993-07-15 Feige Gmbh, Abfuelltechnik, 2060 Bad Oldesloe, De
FR2711610B1 (en) 1993-10-29 1996-02-02 Andre J J Graffin Method of filling a container with a reference net weight.

Also Published As

Publication number Publication date
ES2226889T3 (en) 2005-04-01
US6334471B1 (en) 2002-01-01
ATE276196T1 (en) 2004-10-15
BR0012587A (en) 2002-04-09
EP1196346A1 (en) 2002-04-17
JP2003505674A (en) 2003-02-12
FR2797258B1 (en) 2001-10-05
FR2797258A1 (en) 2001-02-09
PT1196346E (en) 2005-01-31
DE60013835D1 (en) 2004-10-21
WO2001005698A1 (en) 2001-01-25
DK1196346T3 (en) 2005-01-17
DE60013835T2 (en) 2005-10-06

Similar Documents

Publication Publication Date Title
EP1196346B1 (en) Method for filling a container
EP0524850B1 (en) Weight-responsive dosage method for filling containers
EP0724528B2 (en) Method of filling a container with a product having a net set weight
EP0406092B1 (en) Device for filling containers with weighted measures
FR2520108A1 (en) METHOD AND INSTALLATION FOR DETERMINING VALUES DEPENDING ON THE MASS FLOW OF A DOSING MATERIAL
CH632718A5 (en) WEIGHT SUPPLY APPARATUS.
FR2628835A1 (en)
FR2596886A1 (en) METHOD FOR CONTROLLING AND CONTROLLING THE FLOW RATE, IN PARTICULAR FOR SCALES
FR2505757A1 (en) ANTI-LOCK CONTROL SYSTEM FOR VEHICLE WHEELS
WO2000023373A1 (en) Method for controlling the filling of containers with a flowable product and filling installation implementing said method
FR2496627A1 (en) Filling-level control for bottle-filling machine - adjusts height of filling head to type of bottle using data processor (NL 16.07.82)
CH676749A5 (en)
EP0080406B1 (en) Method and apparatus for interrogating a combustible gas concentration sensor
FR2634382A1 (en) ARTIFICIAL PANCREAS
EP0086145B1 (en) Flow meter and device to mix in an additive with a fluid comprising such a flow meter
FR2525359A1 (en) METHOD AND DEVICE FOR ATTITUDE REGULATION OF AN ARTIFICIAL TERRESTRIAL SATELLITE
FR2597025A1 (en) Process and apparatus for laying down, by extrusion, a bead of pasty material onto a support
FR2862714A1 (en) Injection system monitoring method for e.g. heat engine, involves opening and closing dosage unit during usage of signal to find instant from which flow of fuel across pressure regulation valve starts to reduce, for detecting fault in unit
EP0403401B1 (en) Method to control ultrafiltration and device for carrying out this method
FR2716969A1 (en) Device for weighing groups of cigarettes from a cigarette manufacturing machine.
EP1797751B1 (en) Spreader
CH639007A5 (en) FILTER BAND MACHINER.
EP4292717A1 (en) Coating product application installation and method for controlling such an installation
EP0438202A1 (en) Spreader for spreadable material
EP0360693A1 (en) Device for measuring the firmness of a deformable object

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20020115

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: FRENCH

REF Corresponds to:

Ref document number: 60013835

Country of ref document: DE

Date of ref document: 20041021

Kind code of ref document: P

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: BOVARD AG PATENTANWAELTE

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20041108

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

REG Reference to a national code

Ref country code: GR

Ref legal event code: EP

Ref document number: 20040404350

Country of ref document: GR

REG Reference to a national code

Ref country code: PT

Ref legal event code: SC4A

Effective date: 20041117

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20040915

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2226889

Country of ref document: ES

Kind code of ref document: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20050703

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050703

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050731

26N No opposition filed

Effective date: 20050616

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Owner name: S.E.R.A.C. GROUP

Free format text: S.E.R.A.C. GROUP#ROUTE DE MAMERS#72400 LA FERTE-BERNARD (FR) -TRANSFER TO- S.E.R.A.C. GROUP#ROUTE DE MAMERS#72400 LA FERTE-BERNARD (FR)

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 60013835

Country of ref document: DE

Representative=s name: SCHAUMBURG & PARTNER PATENTANWAELTE GBR, DE

Ref country code: DE

Ref legal event code: R082

Ref document number: 60013835

Country of ref document: DE

Representative=s name: SCHAUMBURG UND PARTNER PATENTANWAELTE MBB, DE

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 17

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 18

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PT

Payment date: 20190621

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20190719

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20190719

Year of fee payment: 20

Ref country code: ES

Payment date: 20190822

Year of fee payment: 20

Ref country code: IT

Payment date: 20190730

Year of fee payment: 20

Ref country code: IE

Payment date: 20190723

Year of fee payment: 20

Ref country code: FR

Payment date: 20190719

Year of fee payment: 20

Ref country code: DK

Payment date: 20190723

Year of fee payment: 20

Ref country code: DE

Payment date: 20190719

Year of fee payment: 20

Ref country code: FI

Payment date: 20190722

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20190718

Year of fee payment: 20

Ref country code: GR

Payment date: 20190719

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20190722

Year of fee payment: 20

Ref country code: GB

Payment date: 20190719

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20190719

Year of fee payment: 20

REG Reference to a national code

Ref country code: DE

Ref legal event code: R071

Ref document number: 60013835

Country of ref document: DE

REG Reference to a national code

Ref country code: DK

Ref legal event code: EUP

Expiry date: 20200703

REG Reference to a national code

Ref country code: NL

Ref legal event code: MK

Effective date: 20200702

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Expiry date: 20200702

Ref country code: IE

Ref legal event code: MK9A

REG Reference to a national code

Ref country code: FI

Ref legal event code: MAE

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK07

Ref document number: 276196

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200703

REG Reference to a national code

Ref country code: BE

Ref legal event code: MK

Effective date: 20200703

REG Reference to a national code

Ref country code: SE

Ref legal event code: EUG

REG Reference to a national code

Ref country code: SE

Ref legal event code: EUG

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20201026

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20200703

Ref country code: PT

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20200713

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20200702

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20200704